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Determine the specific volume of superheated water vapor at \(15 \mathrm{MPa}\) and \(350^{\circ} \mathrm{C}\), using \((a)\) the ideal-gas equation, ( \(b\) ) the generalized compressibility chart, and (c) the steam tables. Also determine the error involved in the first two cases.

Short Answer

Expert verified
Answer: The specific volume using the ideal-gas equation is 0.01915 m³/kg, using the generalized compressibility chart is 0.01723 m³/kg, and using steam tables is 0.01717 m³/kg. The error involved in the ideal-gas equation is 11.52%, and the error in the generalized compressibility chart method is 0.35%.

Step by step solution

01

Specific volume using the ideal-gas equation

To determine the specific volume using the ideal-gas equation, we use the following equation: \(v = \frac{RT}{P}\) where \(v\) is the specific volume, \(R\) is the specific gas constant for water vapor, \(T\) is the temperature in Kelvin, and \(P\) is the pressure. First, we need to convert the given temperature and pressure to appropriate units: Temperature: \(T = 350^{\circ}C = 350 + 273.15 = 623.15 K\) Pressure: \(P = 15 \, \text{MPa} = 15 \times 10^6 \, \text{Pa}\) R = 461.5 J/(kg*K) (Specific gas constant for water vapor) Now, we can calculate the specific volume using the ideal-gas equation: \(v = \frac{RT}{P} = \frac{461.5 \, \text{J/(kg*K)} \times 623.15 \, \text{K}}{15 \times 10^6 \, \text{Pa}} = 0.01915\,\text{m}^3/\text{kg}\)
02

Specific volume using the generalized compressibility chart

To determine the specific volume using the generalized compressibility chart, we need to find the compressibility factor, \(Z\), at the given reduced pressure and reduced temperature. The reduced pressure and temperature can be calculated using: \(P_r = \frac{P}{P_c}\) \(T_r = \frac{T}{T_c}\) For water vapor, the critical pressure \(P_c = 22.064 \, \text{MPa}\) and the critical temperature \(T_c = 647.3 \, \text{K}\). We can now determine the reduced pressure and temperature: \(P_r = \frac{15 \, \text{MPa}}{22.064 \, \text{MPa}} = 0.68\) \(T_r = \frac{623.15 \, \text{K}}{647.3 \, \text{K}} = 0.963\) Using the generalized compressibility chart, we find the compressibility factor \(Z\) at these values to be approximately \(Z=0.9\). Now, we can find the specific volume using the following equation: \(v = Z \frac{RT}{P} = 0.9 \times \frac{461.5 \, \text{J/(kg*K)} \times 623.15 \, \text{K}}{15 \times 10^6 \, \text{Pa}} = 0.01723 \, \text{m}^3/\text{kg}\)
03

Specific volume using steam tables

Using steam tables, we look up the specific volume at the given pressure and temperature. For water vapor at \(15 \, \text{MPa}\) and \(350^{\circ} C\), we find the specific volume to be: \(v = 0.01717 \, \text{m}^3/\text{kg}\)
04

Error calculation

Now we can determine the error involved in the ideal-gas equation and the generalized compressibility chart: Error in ideal-gas equation: \(error = \frac{|v_{\text{ideal}}-v_{steam}|}{v_{steam}} \times 100 = \frac{|0.01915-0.01717|}{0.01717} \times 100 = 11.52 \%\) Error in generalized compressibility chart: \(error = \frac{|v_{\text{chart}}-v_{steam}|}{v_{steam}} \times 100 = \frac{|0.01723-0.01717|}{0.01717} \times 100 = 0.35 \%\) The error in the ideal-gas equation method is 11.52%, and the error in the generalized compressibility chart method is 0.35%.

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Most popular questions from this chapter

The gage pressure of an automobile tire is measured to be \(200 \mathrm{kPa}\) before a trip and \(220 \mathrm{kPa}\) after the trip at a location where the atmospheric pressure is 90 kPa. Assuming the volume of the tire remains constant at \(0.035 \mathrm{m}^{3},\) determine the percent increase in the absolute temperature of the air in the tire.

What is the principle of corresponding states?

Is it true that it takes more energy to vaporize \(1 \mathrm{kg}\) of saturated liquid water at \(100^{\circ} \mathrm{C}\) than it would at \(120^{\circ} \mathrm{C} ?\)

A rigid tank initially contains \(1.4-\mathrm{kg}\) saturated liquid water at \(200^{\circ} \mathrm{C}\). At this state, 25 percent of the volume is occupied by water and the rest by air. Now heat is supplied to the water until the tank contains saturated vapor only. Determine \((a)\) the volume of the \(\tan \mathrm{k},(b)\) the final temperature and pressure, and \((c)\) the internal energy change of the water.

Water initially at 200 kPa and \(300^{\circ} \mathrm{C}\) is contained in a piston-cylinder device fitted with stops. The water is allowed to cool at constant pressure until it exists as a saturated vapor and the piston rests on the stops. Then the water continues to cool until the pressure is \(100 \mathrm{kPa}\). On the \(T\) -v diagrams sketch, with respect to the saturation lines, the process curves passing through both the initial, intermediate, and final states of the water. Label the \(T, P\) and \(v\) values for end states on the process curves. Find the overall change in internal energy between the initial and final states per unit mass of water.

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